Claims
- 1. A process for preparing a heat-curable multilayer composite sheet, which comprises coating a layer-forming material containing a normally solid or liquid free radical reactive unsaturated compound on a first strippable sheet to form an unsaturated compound material layer on the first strippable sheet, coating another layer-forming material containing a normally solid or liquid free radical initiator on a second strippable sheet to form a free radical initiator layer on the second strippable sheet, bringing the unsaturated compound material layer into contact with the free radical initiator layer, and bonding them to each other at a temperature at which the free radical initiator layer does not lose its free radical reaction initiating ability, essentially no free radical initiator being in said layer-forming material and essentially no free radical reactive unsaturated compound being in said another layer-forming material.
- 2. The process of claim 1, wherein said strippable sheets are materials selected from the group consisting of glassine paper treated with silicone resin, a polyethylene film treated with silicone resin, a polyester film treated with silicone resin, a polytetrafluoroethylene film or a metal sheet having a surface treated with a silicone resin by a mold releasing method.
- 3. The process of claim 1, wherein said unsaturated compound is selected from the group consisting of
- (i) an unsaturated polymer containing at least two double bonds per molecule;
- (ii) a mixture of an unsaturated polymer containing at least two double bonds per molecule and an unsaturated monomer; or
- (iii) a mixture of an unsaturated polymer containing at least two double bonds per molecule and an unsaturated polymer containing one double bond per molecule.
- 4. The process of claim 3, wherein the unsaturated compound is said mixture (iii) and the amount of the double bonds in the unsaturated compound is about 10.sup.19 to about 10.sup.21 per gram, and the proportion of the double bonds in the polymer containing at least two double bonds per molecule is at least 0.1% based on the total double bond content.
- 5. The process of claim 4, wherein the proportion of double bonds in the polymer containing at least two double bonds per molecule is at least about 1.0% based on the total double bond content.
- 6. The process of claim 4, wherein the proportion of double bonds in the polymer containing at least two double bonds per molecule is at least 10% but less than 100% based on the total double bond content.
- 7. The process of claim 3, wherein said unsaturated polymer containing at least two double bonds per molecule is selected from the group consisting of
- (a) an acryclic unsaturated polymer of the formula ##STR2## wherein X is a hydrogen atom or a methyl group, and Y is a residue of a member selected from the group consisting of polyesters, polyurethanes, epoxy compounds and polyglycols, which has a molecular weight of not more than about 5,000;
- (b) an unsaturated polyester resin having a molecular weight of about 1,000 to about 50,000; or
- (c) an unsaturated polymer precursor having a molecular weight of about 100 to about 5,000.
- 8. The process of claim 7, wherein the unsaturated polymer containing at least two double bonds per molecule is an acrylic unsaturated polymer of the formula: ##STR3## wherein X is a hydrogen atom or a methyl group, and Y is a residue of a member selected from the group consisting of polyesters, polyurethanes, epoxy compounds and polyglycols, which has a molecular weight of not more than about 5,000.
- 9. The process of claim 8, wherein the unsaturated compound comprises the acrylic unsaturated polymer and about 0.1 to about 100% by weight, based on the polymer, of an unsaturated monomer.
- 10. The process of claim 1, wherein the amount of the initiator, in terms of the number of active free radicals generated from the initiator, is about 0.1 to about 1,000 per 1,000 double bonds of the unsaturated compound per unit area of the composite sheet.
- 11. The process of claim 1, wherein the amount of the initiator, in terms of the number of active free radicals generated from the initiator, is 1 to 100 per 1,000 double bonds of the unsaturated compound per unit area of the composite sheet.
- 12. The process of claim 1, wherein the amount of the initiator, in terms of the number of active free radicals generated from the initiator, is 5 to 50 per 1,000 double bonds of the unsaturated compound per unit area of the composite sheet.
- 13. The process of claim 1, wherein the layer on the first strippable sheet further comprises a non-reactive carrier.
- 14. The process of claim 13 wherein the amount of the non-reactive carrier is not more than about 500% by weight of the unsaturated compound.
- 15. The process of claim 13, wherein the amount of the non-reactive carrier is not more than 200% by weight of the unsaturated compound.
- 16. The process of claim 13, wherein the amount of the non-reactive carrier is not more than 100% by weight based on the unsaturated compound.
- 17. The process of claim 13, wherein the non-reactive carrier is a hot-melt adhesive.
- 18. The process of claim 1, wherein the layer on the second strippable sheet further comprises a non-reactive carrier.
- 19. The process of claim 18, wherein the amount of the non-reactive carrier is not more than about 2,000% by weight based on the initiator.
- 20. The process of claim 18, wherein the amount of the non-reactive carrier is not more than 1,000% by weight based on the initiator.
- 21. The process of claim 18, wherein the amount of the non-reactive carrier is not more than 100% by weight based on the initiator.
- 22. The process of claim 1, wherein the initiator is a peroxide radical initiator, an azo radical initiator or an inorganic radical initiator.
- 23. The process of claim 22, wherein the initiator is a peroxide radical initiator and is selected from the group consisting of a peroxide, a peracid or a peroxy ester.
- 24. The process of claim 1, wherein the initiator is benzoyl peroxide.
- 25. The process of claim 1, wherein the unsaturated compound layer and the initiator layer both have a thickness of about 0.01 to about 1.0 mm.
- 26. The process of claim 1, wherein said temperature at which the free radical initiator layer does not lose its free radical reaction initiating ability is from about 40 to about 70.degree. C.
- 27. The process of claim 1, wherein the layer on said first strippable sheet is heated to about 40 to about 70.degree. C. rendering it tacky prior to said bonding.
- 28. The process of claim 27, wherein said bonding is accomplished by passing said two layers between two rolls having a roll pressure of about 0.5 to about 10 kg/cm.sup.2.
- 29. The process of claim 3, wherein said unsaturated monomer in mixture (ii) is selected from the group consisting of triallyl cyanurate, tolylene diallyl carbamate, diallyl isocyanurate, N-methylol acrylamide, acrylamide, methylacrylamide, N-tertiary butyl acrylamide, diacetone acrylamide, triacryl formal, ethyl acrylate, butyl acrylate, vinyl stearate, N-vinyl carbazole, divinylbenzene, divinyl ethylene glycol, maleimide, dimethyl itaconate, acenaphthylene, diallyl phthalate or trimethylol propane trimethacrylate.
- 30. The process of claim 7, wherein said polymer precursor is a diallyl phthalate prepolymer.
- 31. The process of claim 3, wherein said unsaturated compound is mixture (ii) and the amount of unsaturated monomer in the mixture is about 0.1 to about 100% by weight based on the polymer.
- 32. The process of claim 31, wherein said amount is about 1 to about 30% by weight.
- 33. The process of claim 7, wherein said unsaturated polyester resin (b) is synthesized by esterifying an acid component composed of at least one unsaturated carboxylic acid and a saturated polybasic carboxylic acid with a polyhydric alcohol and wherein said unsaturated polymer precursor (c) is synthesized by polymerizing, to an about 2 to about 50 degree or polymerization, one of more monomers having two or more double bonds per molecule in which at least one double bond per molecule remains in the precursor.
- 34. The process of claim 13, wherein said non-reactive carrier is a thermoplastic resin or a rubber.
- 35. A process for preparing a heat-curable multilayer composite sheet, which comprises coating a layer-forming material containing a normally solid or liquid free radical reactive unsaturated compound on a first strippable sheet to form an unsaturated compound material layer on the first strippable sheet, coating another layer-forming material containing a normally solid or liquid free radical initiator on a second strippable sheet to form a free radical initiator layer on the second strippable sheet, bringing the unsaturated compound material layer into contact with the free radical initiator layer, and bonding them to each other (a) without heating when one of the layers is tacky at room temperature or (b) when neither of said layers is tacky at room temperature, by heating at least one of said layers to a tackifying temperature at which the free radical initiator layer does not lose its free radical reaction initiating ability, essentially no free radical initiator being in said layer-forming material and essentially no free radical reactive unsaturated compound being in said another layer-forming material.
- 36. The process of claim 35 wherein bonding step (a) is used and the unsaturated compound material layer is tacky.
- 37. The process of claim 35 wherein bonding step (b) is used and only the unsaturated compound material layer is rendered tacky by heating.
Priority Claims (2)
Number |
Date |
Country |
Kind |
50/37611 |
Mar 1975 |
JPX |
|
50/46663 |
Apr 1975 |
JPX |
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Parent Case Info
This application is a continuation application of Ser. No. 877,523, filed Feb. 13, 1978, now abandoned, in turn a divisional application of Ser. No. 655,198, filed Feb. 4, 1976, now U.S. Pat. No. 4,091,157.
US Referenced Citations (10)
Foreign Referenced Citations (1)
Number |
Date |
Country |
1254007 |
Nov 1967 |
DEX |
Divisions (1)
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Number |
Date |
Country |
Parent |
655198 |
Feb 1976 |
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Continuations (1)
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Number |
Date |
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Parent |
877523 |
Feb 1978 |
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